9003-20-7Relevant articles and documents
Catalytic Hydrogenation of Trivinyl Orthoacetate: Mechanisms Elucidated by Parahydrogen Induced Polarization
Pravdivtsev, Andrey N.,Brahms, Arne,Kienitz, Stephan,S?nnichsen, Frank D.,H?vener, Jan-Bernd,Herges, Rainer
, p. 370 - 377 (2021/02/09)
Parahydrogen (pH2) induced polarization (PHIP) is a unique method that is used in analytical chemistry to elucidate catalytic hydrogenation pathways and to increase the signal of small metabolites in MRI and NMR. PHIP is based on adding or exchanging at least one pH2 molecule with a target molecule. Thus, the spin order available for hyperpolarization is often limited to that of one pH2 molecule. To break this limit, we investigated the addition of multiple pH2 molecules to one precursor. We studied the feasibility of the simultaneous hydrogenation of three arms of trivinyl orthoacetate (TVOA) intending to obtain hyperpolarized acetate. It was found that semihydrogenated TVOA underwent a fast decomposition accompanied by several minor reactions including an exchange of geminal methylene protons of a vinyl ester with pH2. The study shows that multiple vinyl ester groups are not suitable for a fast and clean (without any side products) hydrogenation and hyperpolarization that is desired in biochemical applications.
Catalyst for acetylene method vinyl acetate synthesis
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Paragraph 0043-0245, (2021/11/10)
The invention relates to a catalyst for acetylene-method vinyl acetate synthesis and a preparation method thereof, and mainly solves the problem that by-product benzene content in the prior art is high. The catalyst comprises a carrier and an active component loaded on the carrier, wherein the active component comprises zinc acetate, and the carrier is activated carbon. The content of zinc acetate in the catalyst is 25 - 50g/L, the zinc acetate particle size is 3.0 - 5.0 nm, the problem is well solved, and the catalyst can be used in industrial production of acetylene-method vinyl acetate.
PROCESS TO PRODUCE ETHYLENE AND VINYL ACETATE MONOMER AND DERIVATIVES THEREOF
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Page/Page column 57-59, (2019/10/04)
A method that includes (a) providing a stream containing ethane and oxygen to an ODH reactor; (b) converting a portion of the ethane to ethylene and acetic acid in the ODH reactor to provide a stream containing ethane, ethylene, acetic acid, oxygen and carbon monoxide; (c) separating a portion of the acetic acid from the stream to provide an acetic acid stream and a stream containing ethane, ethylene, oxygen and carbon monoxide; (d) providing the stream to a CO Oxidation Reactor containing a catalyst that includes a group 11 metal to convert carbon monoxide to carbon dioxide and reacting acetylene to produce a stream containing ethane, ethylene and carbon dioxide; and (e) providing a portion of the stream and a portion of the acetic acid stream to a third reactor containing a catalyst that includes a metal selected from group 10 and group 11 metals to produce vinyl acetate.
Post-gilding of PD-AU-coated shell catalysts
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Page/Page column 16; 17, (2018/02/28)
The invention relates to a method for producing a shell catalyst that is suitable for producing vinyl acetate monomer (VAM). The invention further relates to a shell catalyst that is obtainable by the method according to the invention and to the use of the shell catalyst according to the invention for producing VAM.
HIGH PORE VOLUME ALUMINA SUPPORTED CATALYST FOR VINYL ACETATE MONOMER (VAM) PROCESS
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Paragraph 0082-0084, (2018/05/26)
Disclosed is a supported catalyst for the preparation of vinyl acetate monomer (VAM), a process for preparing a catalyst comprising an extruded alumina support, and a catalytic process for the manufacturing vinyl acetate using the supported catalyst. Specifically, it is shown that for activated palladium-gold VAM catalysts prepared using extruded alumina supports, enhanced performance is demonstrated with increased pore volume of the support, and the gas hourly space velocity (GHSV, hr?1), which was found to significantly increase the space time yield as GHSV increased as compared to the non-extruded alumina supported catalysts.
Nanostructured Pd?Cu Catalysts Supported on Zr?Al and Zr?Ti for Synthesis of Vinyl Acetate
Gonzalez Caranton, Alberth Renne,Dille, Jean,Barreto, Jade,Stavale, Fernando,Pinto, José Carlos,Schmal, Martin
, p. 5256 - 5269 (2018/11/10)
Renewable ethylene can be obtained by dehydration of bio-ethanol and used for production of vinyl acetate (VAM) through reaction with acetic acid (AcOH), using Pd?Cu catalysts. In the present manuscript, structural characterizations of Pd?Cu/ZrO2 catalysts show that these systems present cubic structure with different spatial distributions. Particularly, it is shown that combustion of ethylene and acetic acid can be inhibited below 180 °C, maximizing the rates of VAM formation, when the catalysts are modified with Ti+4. The effects of AcOH concentration on rates of VAM formation show that higher AcOH concentrations favor the formation of undesired byproducts, while lower AcOH concentrations favor effects related to O2 mobility, which can lead to surface decomposition. VAM formation is favored, with selectivities ranging from 0.8 to 1.0. XPS results indicate the existence of metallic Pd, CuO species and Zr species, in agreement with IR results. DRIFTS results also show that different Pd-acetate intermediates can be present, depending on the electronic effects associated to Pd?Cu and Zr species.
By preparing vinyl acetate ethylene diacetate cracking method
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Paragraph 0009; 0019; 0020; 0021; 0022-0027, (2017/04/28)
The invention relates to a method for preparing vinyl acetate (VAC) from ethylidene diacetate (EDA) through pyrolysis. The method mainly comprises the following step: in the presence of a catalyst, performing thermal pyrolysis on EDA so as to obtain VAC. The method is characterized in that the catalyst is aluminum trichloride modified macropore styrene cation exchange resin, and aluminum trichloride accounts for 0.1-3.0wt% of the total weight of the catalyst. When VAC is prepared by using the method provided by the invention, not only is the VAC easily separated from the catalyst, but also the conversion rate of EDA can be increased, and the selectivity of VAC can be relatively greatly improved.
HIGH GEOMETRIC SURFACE AREA CATALYSTS FOR VINYL ACETATE MONOMER PRODUCTION
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Paragraph 0050, (2017/02/09)
A catalyst includes a support, where the support includes an external surface, about 60 wt% to about 99 wt% silica, and about 1.0 wt% to about 5.0 wt% alumina. A catalytic layer is disposed within the support adjacent to the external surface, where the catalytic layer further includes Pd, Au, and potassium acetate (KOAc). In the catalyst, (a) the KOAc is from about 60 kg/m3 to about 150 kg/m3 of the catalyst; or (b) the catalytic layer has an average thickness from about 50 μm to about 150 μm; or (c) both (a) and (b). The catalyst also possesses a Brunauer-Emmett-Teller surface area of about 130 m2/g to about 300 m2/g and a geometric surface area per packed bed volume from about 550 m2/m3 to about 1500 m2/m3. The catalyst is highly active for the synthesis of vinyl acetate monomer and exhibits a high selectivity for vinyl acetate monomer.
PROCESS FOR THE PREPARATION OF VINYL ACETATE
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Paragraph 0048, (2016/03/13)
A process for the preparation of vinyl acetate by a heterogeneously catalysed, continuous gas-phase reaction of ethylene, acetic acid and oxygen in a reactor, where process heat liberated during the reaction is removed from the reactor by means of heat exchange with water, generating intrinsic steam, the product mixture leaving the reactor and comprising ethylene, vinyl acetate, acetic acid, water, carbon dioxide and inert gases is separated by distillation using one or more azeotrope columns and/or one or more pure distillation columns, wherein at least one azeotrope column and/or pure distillation column contains packings, and intrinsic steam is used at least partially for introducing energy into the thus-equipped azeotrope columns and/or pure distillation columns.
ELECTROLESS DEPOSITION OF AU-PD BIMETALLIC CATALYSTS FOR ALKENYL ACETATE PRODUCTION
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Page/Page column 16, (2016/12/26)
The present invention relates to a process for the preparation of a Au-Pd bimetallic shell-type catalyst, comprising the following steps: a. providing a solid, shaped body catalyst support, b. contacting the support with two solutions, one solution containing Au ions in an amount of from 0.1-10 wt% and the other solution containing Pd ions in an amount of from 0.1-10 wt%, with the proviso that the weight ratio of Pd:Au is in the range of from 0.2:1 to 4:1. c. reducing the plated support with hydrogen to obtain the Au-Pd bimetallic shell-type pre-catalyst, d. contacting the Au-Pd bimetallic pre-catalyst with an aqueous potassium acetate solution with a content of potassium in the range of from 0.1-10 wt%, e. drying to obtain the Au-Pd bimetallic shell-type catalyst. The invention further relates to a process for the production of alkenyl acetates, applying the Au-Pd bimetallic catalyst.